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WO1992001394A1 - Moisture barrier film - Google Patents

Moisture barrier film Download PDF

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Publication number
WO1992001394A1
WO1992001394A1 PCT/GB1991/001244 GB9101244W WO9201394A1 WO 1992001394 A1 WO1992001394 A1 WO 1992001394A1 GB 9101244 W GB9101244 W GB 9101244W WO 9201394 A1 WO9201394 A1 WO 9201394A1
Authority
WO
WIPO (PCT)
Prior art keywords
film
film according
edible
pastry
protein
Prior art date
Application number
PCT/GB1991/001244
Other languages
French (fr)
Inventor
Alistair Gilmour Tanner
Wilson Harvey
Original Assignee
Devro Limited
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Devro Limited filed Critical Devro Limited
Priority to JP03512374A priority Critical patent/JP3091487B2/en
Priority to EP91913611A priority patent/EP0550445B1/en
Priority to AU82218/91A priority patent/AU644463B2/en
Priority to DE69110894T priority patent/DE69110894T2/en
Priority to BR919106666A priority patent/BR9106666A/en
Publication of WO1992001394A1 publication Critical patent/WO1992001394A1/en
Priority to GB9301414A priority patent/GB2262245B/en

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Classifications

    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23PSHAPING OR WORKING OF FOODSTUFFS, NOT FULLY COVERED BY A SINGLE OTHER SUBCLASS
    • A23P20/00Coating of foodstuffs; Coatings therefor; Making laminated, multi-layered, stuffed or hollow foodstuffs
    • A23P20/20Making of laminated, multi-layered, stuffed or hollow foodstuffs, e.g. by wrapping in preformed edible dough sheets or in edible food containers
    • AHUMAN NECESSITIES
    • A21BAKING; EDIBLE DOUGHS
    • A21DTREATMENT OF FLOUR OR DOUGH FOR BAKING, e.g. BY ADDITION OF MATERIALS; BAKING; BAKERY PRODUCTS
    • A21D13/00Finished or partly finished bakery products
    • A21D13/20Partially or completely coated products
    • A21D13/26Partially or completely coated products the coating forming a barrier against migration
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23PSHAPING OR WORKING OF FOODSTUFFS, NOT FULLY COVERED BY A SINGLE OTHER SUBCLASS
    • A23P20/00Coating of foodstuffs; Coatings therefor; Making laminated, multi-layered, stuffed or hollow foodstuffs
    • A23P20/10Coating with edible coatings, e.g. with oils or fats
    • A23P20/105Coating with compositions containing vegetable or microbial fermentation gums, e.g. cellulose or derivatives; Coating with edible polymers, e.g. polyvinyalcohol

Definitions

  • This invention relates to a moisture barrier film, and more particularly to an edible film which is suitable for use as a moisture barrier in food products.
  • Collagen a naturally occurring connective tissue protein
  • Films of this type are disclosed, for example, in US-A-3664844 and US-A-3529530.
  • the benefits of using collagen for the manufacture of food films are that it is a natural product, the chemistry of which is well understood (see Ramachandran, G.N. & Reddi, A.H. (eds.) (1976) "Biochemistry of Collagen", pub. Plenum Press, NY. & London) , it can be readily comminuted and converted to a viscous gel or mass and it can be extruded in a number of forms including films (see Chvapil, M.
  • SUBSTITUTE SHEET are also machinable (in the sense that they can readily be reeled, cut and handled by machinery) , and they may be used in the preparation of heat-sealed pouches.
  • Moisture-impermeable films have also been widely used in the food industry. These include, for example, the plastics food wrappings already mentioned above. Much earlier examples include the use by the ancient Chinese of edible wax coatings on fruit to prevent drying during storage and the use of fat wrappings (lardings) in 16th century England.
  • Japanese Patent No. 301387 (Kanebo K.K.) describes a zeolite-based non-edible film with moisture absorbing ability which is claimed to extend shelf-life.
  • EP-A-0269460 describes a collagen film coated with a fine layer of emulsified animal fat as a wrap for meat products which prevents moisture loss. This product is a combination of the film wrap and larding techniques and is only applicable to meat "logs" or round joints.
  • a film comprising an edible protein and an edible polysaccharide, said film having a coating of an edible hydrophobic material on at least a portion of a surface thereof.
  • the invention thus provides an edible film which is at least partially moisture-impermeable.
  • the film is coated with the hydrophobic material over substantially the whole (for example, greater than 95%) of at least one surface, such that the film is substantially completely moisture-impermeable.
  • the film may have a moisture permeability of less than 5g/m 2 /day/mm Hg, and more preferably less than 2 g/m/day/mm Hg. If desired, the film may be coated with the same or different hydrophobic materials on the two major surfaces thereof.
  • the moisture permeability of the films of the invention may be measured by maintaining a difference in water vapour pressure across the film, and then measuring the mass of water which passes across the film per unit area.
  • a suitable technique (and the one used herein) is that described by Kester & Fennema, (1989) J. Food Sci. 54, p.1384, modified in that water vapour pressure in the container is maintained at zero by means of anhydrous silica gel, rather than anhydrous calcium chloride.
  • the film is sealed over 100ml glass jars each containing approximately 20g of preweighed silica gel, and exposed to a saturated
  • the edible, moisture-impermeable films of the invention are of value in a variety of applications in the food industry.
  • One such application is in the manufacture of foods which contain both wet and dry domains. Examples of such foods include most bakery, pie-type products (such as quiche lorraine, meat pies, fruit pies and pasties) , and also pizzas.
  • a quiche filling may typically have a water activity (Aw) of 0.97 - 0.99, while the pastry base may have a water activity of 0.92 to 0.98.
  • Aw water activity
  • the pastry base may have a water activity of 0.92 to 0.98.
  • Such products it is common in industry for the filling and pastry to be cooked together in the final product. Such products, therefore, have wet and dry domains in close contact and this can cause problems on storage.
  • Moisture from the wet domain can easily migrate into the dry domain (the pastry) , thus wetting it and making it more susceptible to microbial spoilage and at the same time making it organoleptically less acceptable. Such reactions cause a lowering of the viable shelf-life of pies and related products, so that, for example, some superior products of this type may have a chilled shelf-life of only 24 hours.
  • the film of the present invention providing as it does an effective barrier between the wet and dry domains of mixed food products, considerably enhances the shelf-life of such products.
  • the protein component of the film of the invention is important because it helps to maintain the integrity of the film during cooking, so that the moisture-barrier properties are retained even after cooking. This is in contrast to the fatty acid/modified cellulose films of the prior art, which are dissipated on cooking, and which are therefore useful as moisture barriers only for uncooked products. Moreover, the films of the invention are extrudable, and have better handling properties (including increased tensile strength
  • the films of the invention are generally undetectable (whether visually or organoleptically) in the cooked products. Moreover, the films of the invention are of low cost and are readily handled by machinery.
  • films of the invention include the formation of pouches which can be used for portion control in the manufacture of pies and similar food products.
  • the films may be heat-sealable.
  • the edible protein which is used in the film of the invention is preferably insoluble and fibrous, but globular proteins such as casein, albumen and blood proteins may also be used.
  • suitable fibrous proteins are collagen, keratin and elastin, of which collagen is preferred.
  • the protein may be used in its natural form, or - it may be physically or chemically modified prior to use.
  • the fibre length of a fibrous protein may be reduced to less than 0.1mm by physical means such as by forming a fibre gel and then homogenising the gel.
  • Chemical modification of the protein may include (a) solubilisation by proteolysis (using, for example, pepsin) , (b) cross-linking by agents such as aldehydes (e.g. glutaraldehyde or reducing sugars) , and aluminium salts, (c) denaturation by heating to induce partial or complete gelatinisation, and (d) hydrolysis with acid or alkali.
  • aldehydes e.g. glutaraldehyde or reducing sugars
  • aluminium salts e.g. glutaraldehyde or reducing sugars
  • denaturation by heating induced partial or complete gelatinisation
  • hydrolysis with acid or alkali e.g. glutaraldehyde or reducing sugars
  • Two or more such chemical modifications may be used in combination.
  • collagen may be hydrolysed with acid or alkali to form gelatin, and subsequently cross- linked to reduce its solubility during cooking.
  • collagen When collagen is used as the edible protein, it may suitably be obtained from limed bovine corium, i.e. the inner layer of the skin of male or female cattle, which has
  • SUBSTITUTE SHEET been dehaired and limed using standard commercial procedures.
  • the material may be supplied as whole hide- sized pieces, or may be substituted by any other bovine corium material from any part of the whole hide, e.g. belly "splits", hide off-cuts.
  • Other hide materials can be substituted for this raw material including the hides of any of the domestic meat animals, e.g. pig, sheep, deer, goat, chicken, turkey and other species commonly used for food in various parts of the world e.g. the skin of fish or kangaroo.
  • the polysaccharide is preferably film-forming and soluble.
  • examples include charged polysaccharides (e.g. pectin, alginates, agars, carageenans, and chitosan) , gums (e.g. arabic, acacia, tragacanth, locust bean and guar) , and modified celluloses (e.g. cellulose ethers such as methylcellulose, ethylcellulose, hydroxymethylcellulose, hydroxyethylcellulose, hydroxypropylmethylcellulose, hydroxypropylethylcellulose and carboxymethylcellulose) .
  • Starches such as corn flour, crystal gumTM, Dry-FlowTM, and National Starch B38TM may alternatively be used.
  • the preferred polysaccharide is hydroxypropylmethylcellulose (HPMC) .
  • the hydrophobic material should preferably be tasteless, odourless, solid at room temperatures, and pliable, resisting cracking and flaking when the coated film is manipulated.
  • Suitable hydrophobic materials include edible oils and waxes, such as coconut oil, palm oil, palm kernel oil, acetylated monoglyceride (Dynacet) , glycerol monostearate, calcium and sodium steroyl lactate, polyglycerol ester and beeswax. Acetylated monoglyceride is preferred.
  • the film will generally contain protein in an amount of from 5 to 75%, more preferably from 15 to 35%, and most preferably from 20 to 30% by weight of protein plus polysaccharide.
  • the film may additionally contain
  • the protein content of the uncoated film will usually be from 3.5 to 60% by weight, more usually from 12 to 25% by weight, and most preferably from 15 to 22.5% by weight.
  • Suitable plasticisers include glycerol, sorbitol and polyethylene glycol, in amounts up to 40% by weight of the uncoated film.
  • the film contains plasticiser in an amount of from 5 to 30% (and more preferably from 20 to
  • Flavourings for the film include artificial and naturally occurring flavours, spices and herbs. Suitable colourings include caramel and other permitted artificial or natural food dyes, and are generally employed in amounts less than 5% by weight of the uncoated film. Preservatives, such as propionic acid, sorbic acid, sodium nitrate and sodium nitrite, will usually constitute less than 1% by weight of the uncoated film.
  • the film may be formed by extrusion from a collagen/polysaccharide gel.
  • the gel preferably has a solids content in the range 2 to 10%, and more preferably in the range 4 to 7%.
  • the gel film is dried by any suitable means, such as by hot air.
  • the film is then brought up to a pH of from 6 to 8 by passage through an atmosphere of ammonia.
  • the hydrophobic material will generally be applied to the film in an amount of from 10 to 50 g/m 2 , and more preferably from 20 to 40 g/m 2 of film surface, to produce a coating which is from 10 to 50 micrometers thick.
  • Suitable coating techniques include dipping and brushing, but it is preferred to apply the coating by means of a heated roller or spray.
  • Figure 1 is a graph showing the results of penetrometer studies of the pastry base of a quiche prepared with the film of the present invention.
  • Figure 2 is a graph showing the effect of the film of the invention on the moisture content of quiche pastry.
  • Limed bovine corium (or other suitable collagen source) is placed in a large rotating vessel, e.g. a stainless steel Challenge-Cooke mixer or any other similar devices for freely mixing the raw material with water and other solvents to aid rapid washing/decalcification.
  • a large rotating vessel e.g. a stainless steel Challenge-Cooke mixer or any other similar devices for freely mixing the raw material with water and other solvents to aid rapid washing/decalcification.
  • deliming agents which remove chemically deposited and chemically bound lime by conversion into readily soluble salts can be utilized, e.g. ammonium sulphate, C0 2 deliming systems, hydrochloric acid, malic acid, acetic acid, lactic acid, citric acid-sodium citrate, or ammonium chloride.
  • the temperature of the system should be less than 20°C.
  • the procedure is continued until the final liquor pH is approximately 4.5 - 5.
  • the hides are then washed in water and drained.
  • the washed hides may then be stored at 2 -10°C or deep frozen until required.
  • the temperature of all solvents at all stages should be less than 20°C.
  • the washed, decalcified and salted raw material is passed through a grinder for initial comminution.
  • the whole pieces of corium are fed continuously into a grinding device such as a Weiler or Wolfking industrial food grinder.
  • SUBSTITUTE SHEET material is passed through a plate or plates with 5mm-10mm holes such that 100% of the material is comminuted into approximately Smm-lOmm sized pieces of wet grind. The temperature of the material should be minimised at this stage. This wet grind is then transferred immediately to the next stage.
  • the grind is pumped with water directly from the Wolfking or Weiler grinder to a hide and water holding tank.
  • the resulting slurry is further comminuted by passing through Karl Schnell Mincemasters using plate sizes in the range of l-5mm or through a Stephan Microcut.
  • the temperature rise is minimised at this stage and the resultant collagen pulp stored in the pulp holding tank.
  • Food grade hydrochloric acid, glycerol, sorbitol and optionally aluminium sulphate are then charged to a second holding tank (Acid Tank) , together with water and ice. Suitable final concentrations in solution of these components are within indicated ranges:
  • the contents of the pulp tank and acid tank are blended together using a Stephan Microcut or similar high shear mixer or a Nauta mixer.
  • the desired gel constituents are obtained and the resultant gel is stored in a blend tank for a minimum of 12 hours.
  • the collagen gel thus obtained from the previous step is mixed in a Giusti pressure/mixing vessel, using iced water for cooling, with a solution of polysaccharide containing sufficient plasticiser to give a final solids content of 3.5% with a ratio of 25:75 collagen:polysaccharide by weight and the same final percentage of plasticiser as in the collagen only gel.
  • Suitable polysaccharides include guar gum, locust bean gum, National Starch B38, crystal gum, "Dry-Flow", corn flour, methyl cellulose and hydroxypropyl methyl cellulose (HPMC) , preferably HPMC.
  • the resulting gel is homogenised using a Cherry Burrell homogeniser with automatic pressure control (34.5 ⁇ 1.4 MPa, ie 5000 ⁇ 200psi, with a minimal temperature rise) and passed into a line tank at a minimum of -730mm Hg via a deaerating distributor.
  • the tank is pressurised to 270 kPa (2.7 Bar) and the gel then passed through two gel filters.
  • Four filter banks are used to allow changing of gel filters - 2 for the first filter (placed in parallel) and 2 for the second filter (placed in parallel) .
  • the first and second filters should be placed in series, and the gel filters should be capable of retaining particles greater than 0.076mm (0.003") .
  • the gel is transferred directly to an extruder.
  • the gel is maintained at a maximum temperature of 19 ⁇ 4°C) and extruded at 345 kPa (50 psi) onto a suitable conveyor, such as a PTFE (polytetrafluorethylene) coated glass fibre belt.
  • a suitable conveyor such as a PTFE (polytetrafluorethylene) coated glass fibre belt.
  • the film is then batch-dried on the conveyor at 45°C for approximately 20 mins.
  • a hydrophobic layer is applied to one surface of the film using a heated roller loaded with the coating material, producing an even coating approximately 12.5 micrometres
  • SUBSTITUTE-SHEET (Dynacet) , glycerol monostearate, calcium and sodium steroyl lactate and polyglycerol ester.
  • Pastry ingredients % w/w
  • the milk was heated to 50°C and the eggs and salt beaten in. 330g or 200g (for smaller quiches) of filling was added to the raw pastry base.
  • the pastry base was first covered with the film of the invention, with the hydrophobic surface uppermost.
  • SUBSTITUTE SHEET quiches were cooked in a preheated oven (190_ >C .) for 25 minutes, then the temperature reduced to 150°C for a further 15 minutes. The quiches were then removed, allowed to stand for 5 minutes, loosely covered with foil then chilled to 2°C in less than 90 minutes.
  • Pastry was made to the recipe described above, and 1400mm diameter aluminium moulds were lined with 4mm thick rolled pastry. 200g of commercial tinned meat filling in gravy was added directly to the pastry shell or retained within an experimental film pouch prior to placing in the shell. A top crust (80g of pastry) was placed on top of the pie. Pies were baked at 175°C for 35-40 minutes, allowed to cool to room temperature, then chilled to 5°C.
  • a characteristic of the pastry base which varies with moisture content is the resistance to deformation under applied pressure. This was measured in 50mm discs cut out of the pastry after removal of the filling, using a Lloyd tensile tester, type 5002, with an 8mm diameter probe attached to a 100 Newton load cell, crosshead speed 25mm per in.
  • the characteristic of the stress/strain curve which was used was the peak height (Fig. 1) , corresponding to "firmness” or resistance to penetration; this was expressed as Newtons (N) .
  • the filling was separated from the pastry base and both were ground to homogeneity. lOg samples were weighed before and after heating at 80°C to constant weight (6h for pastry,
  • a standard triangle taste for sensory difference was used with a randomly selected panel of 24 tasters. Samples of quiches were allocated random codes and the mode of presentation was balanced. Identification of one film- containing sample from two control samples was evaluated using the BS 5929, Part 1 (1980) test.
  • Collagen film with no polysaccharide component shrank during cooking in quiches, exposing the pastry base and allowing penetration of moisture from the filling.
  • Figure 2 illustrates the reduced rate of water migration into the pastry base of a quiche in which the filling and the pastry base are separated by a film comprising collagen and HPMC, with a coating of acetylated monoglyceride.
  • the load/deformation characteristics of the pastry base measured on a tensile tester are shown in Figure 1.
  • the three regions of the curve, A, B and C, are thought to correspond to the three layers of the cooked pastry, described above.
  • the mean rupture load of the pastry decreased during storage, but the decrease was significantly less in quiches incorporating the film when compared with controls (Table 4).
  • the hedonic scores from a taste panel showed a clear improvement in "crispness” of the pastry in quiches with film (Table 5) .
  • the scores indicate consistently higher “brittleness” and lower “softness” for the film-containing samples.
  • the rupture-load of the top and base crusts were measured 24 and 48h after cooking.
  • the pies containing film showed a significantly lower rupture load then controls in the top crusts at both 24 and 48h, but a higher rupture load for the base crust (Table 7) .

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  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Food Science & Technology (AREA)
  • Polymers & Plastics (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Biotechnology (AREA)
  • General Preparation And Processing Of Foods (AREA)
  • Bakery Products And Manufacturing Methods Therefor (AREA)
  • Coating Of Shaped Articles Made Of Macromolecular Substances (AREA)
  • Manufacture Of Macromolecular Shaped Articles (AREA)
  • Laminated Bodies (AREA)
  • Food Preservation Except Freezing, Refrigeration, And Drying (AREA)
  • Formation And Processing Of Food Products (AREA)

Abstract

A moisture barrier film, which is of particular utility in the manufacture of food products, comprises an edible protein and an edible polysaccharide. The film is rendered at least partly moisture-impermeable by the provision of a coating of an edible hydrophobic material on at least a portion of a surface thereof.

Description

MOISTURE BARRIER FILM
This invention relates to a moisture barrier film, and more particularly to an edible film which is suitable for use as a moisture barrier in food products.
Films have been used in food preparations for various reasons for centuries. These applications include the protection of raw and cooked foods, the containment of wet foods and flavours, the separation of wet from dry foods, and the preventing of drying. Examples of the use of natural films in food products are sheep/hog stomach for wrapping comminuted meat as in haggis, and the use of intestines for the manufacture of sausages (see Tannahill, R. , "Food in History", pub. Stein & Day, NY.). In this century, the evolution of plastics films and plastics laminates has allowed a great diversification in food wrapping for the purposes of protection from gross and microbial contamination, inhibition of oxidation, and containment (see Daniels J.A. et al (1985) J. Food Protect. 48. 532; Neilsen, H.J.S. (1983) J. Food Protect. 4_6, 693; and Jantavat, R. & Dawson, L.E. (1980) Poultry Sci. 5_9, 1053) .
Collagen, a naturally occurring connective tissue protein, has been used for the manufacture of food wrapping films on a commercial basis. Films of this type are disclosed, for example, in US-A-3664844 and US-A-3529530. The benefits of using collagen for the manufacture of food films are that it is a natural product, the chemistry of which is well understood (see Ramachandran, G.N. & Reddi, A.H. (eds.) (1976) "Biochemistry of Collagen", pub. Plenum Press, NY. & London) , it can be readily comminuted and converted to a viscous gel or mass and it can be extruded in a number of forms including films (see Chvapil, M. (1979) in "Fibrous Proteins: Scientific, Industrial and Medical Aspects", Vol. 1, pp. 247 et seg (D. Parry & L. Creamer, eds.), pub. Academic Press, NY. & London). Collagen films
SUBSTITUTE SHEET are also machinable (in the sense that they can readily be reeled, cut and handled by machinery) , and they may be used in the preparation of heat-sealed pouches.
International Patent Application No.WO-A-8802991 discloses an alternative film derived from soya protein, casein, albumin or gelatine with polysaccharides such as gum arabic and starch. Such a film, like conventional collagen films, is moisture-permeable.
Moisture-impermeable films have also been widely used in the food industry. These include, for example, the plastics food wrappings already mentioned above. Much earlier examples include the use by the ancient Chinese of edible wax coatings on fruit to prevent drying during storage and the use of fat wrappings (lardings) in 16th century Britain.
More recently, a non-edible, disposable food wrap made from a laminate of saccharides and vinylon film has become available from Showa Denko K.K. of Japan. This film is said to absorb moisture, thereby limiting moisture migration.
Japanese Patent No. 301387 (Kanebo K.K.) describes a zeolite-based non-edible film with moisture absorbing ability which is claimed to extend shelf-life.
Some attempts have also been made in recent years to produce commercially viable films which are both edible and moisture-impermeable. For example, wax and protein sprays have been used in the bakery industry, but with little success.
The combination of fatty acids and modified cellulose with wax layers has been reported for use as a moisture barrier film (see Kamper, S.L & Fennema, 0. (1984) J. Food
Sci. 49, 1478 and 1482; and (1985) J. Food Sci. 50, 382;
Kester, J.J. & Fennema, O. (1989) J. Food Sci. 54, 1383 and
SUBSTITUTESHEET 1390; and Greener, I.K. & Fennema, O. (1989) J. Food Sci. 54, 1393 and 1400) . However, such cellulose-based films have low strength and poor handling characteristics.
EP-A-0269460 describes a collagen film coated with a fine layer of emulsified animal fat as a wrap for meat products which prevents moisture loss. This product is a combination of the film wrap and larding techniques and is only applicable to meat "logs" or round joints.
According to the present invention, there is provided a film comprising an edible protein and an edible polysaccharide, said film having a coating of an edible hydrophobic material on at least a portion of a surface thereof.
The invention thus provides an edible film which is at least partially moisture-impermeable. Preferably, the film is coated with the hydrophobic material over substantially the whole (for example, greater than 95%) of at least one surface, such that the film is substantially completely moisture-impermeable. By way of example, the film may have a moisture permeability of less than 5g/m2/day/mm Hg, and more preferably less than 2 g/m/day/mm Hg. If desired, the film may be coated with the same or different hydrophobic materials on the two major surfaces thereof.
The moisture permeability of the films of the invention may be measured by maintaining a difference in water vapour pressure across the film, and then measuring the mass of water which passes across the film per unit area. A suitable technique (and the one used herein) is that described by Kester & Fennema, (1989) J. Food Sci. 54, p.1384, modified in that water vapour pressure in the container is maintained at zero by means of anhydrous silica gel, rather than anhydrous calcium chloride. The film is sealed over 100ml glass jars each containing approximately 20g of preweighed silica gel, and exposed to a saturated
SUBSTI UTE SHEET atmosphere of water vapour in air in a desiccator at 20 °C. The rate of water vapour transmission through the film is calculated from the weight gain in the silica gel after 48 hrs exposure.
The edible, moisture-impermeable films of the invention are of value in a variety of applications in the food industry. One such application is in the manufacture of foods which contain both wet and dry domains. Examples of such foods include most bakery, pie-type products (such as quiche lorraine, meat pies, fruit pies and pasties) , and also pizzas. A quiche filling may typically have a water activity (Aw) of 0.97 - 0.99, while the pastry base may have a water activity of 0.92 to 0.98. In such products it is common in industry for the filling and pastry to be cooked together in the final product. Such products, therefore, have wet and dry domains in close contact and this can cause problems on storage. Moisture from the wet domain can easily migrate into the dry domain (the pastry) , thus wetting it and making it more susceptible to microbial spoilage and at the same time making it organoleptically less acceptable. Such reactions cause a lowering of the viable shelf-life of pies and related products, so that, for example, some superior products of this type may have a chilled shelf-life of only 24 hours. The film of the present invention, providing as it does an effective barrier between the wet and dry domains of mixed food products, considerably enhances the shelf-life of such products.
The protein component of the film of the invention is important because it helps to maintain the integrity of the film during cooking, so that the moisture-barrier properties are retained even after cooking. This is in contrast to the fatty acid/modified cellulose films of the prior art, which are dissipated on cooking, and which are therefore useful as moisture barriers only for uncooked products. Moreover, the films of the invention are extrudable, and have better handling properties (including increased tensile strength
SUBSTITUTE SHEET and tear strength) in comparison to such prior art films.
Surprisingly, the films of the invention are generally undetectable (whether visually or organoleptically) in the cooked products. Moreover, the films of the invention are of low cost and are readily handled by machinery.
Other applications of the films of the invention include the formation of pouches which can be used for portion control in the manufacture of pies and similar food products. Of particular advantage in this application is that the films may be heat-sealable.
The edible protein which is used in the film of the invention is preferably insoluble and fibrous, but globular proteins such as casein, albumen and blood proteins may also be used. Examples of suitable fibrous proteins are collagen, keratin and elastin, of which collagen is preferred. The protein may be used in its natural form, or - it may be physically or chemically modified prior to use. For example, the fibre length of a fibrous protein may be reduced to less than 0.1mm by physical means such as by forming a fibre gel and then homogenising the gel.
Chemical modification of the protein may include (a) solubilisation by proteolysis (using, for example, pepsin) , (b) cross-linking by agents such as aldehydes (e.g. glutaraldehyde or reducing sugars) , and aluminium salts, (c) denaturation by heating to induce partial or complete gelatinisation, and (d) hydrolysis with acid or alkali. Two or more such chemical modifications may be used in combination. For example, collagen may be hydrolysed with acid or alkali to form gelatin, and subsequently cross- linked to reduce its solubility during cooking.
When collagen is used as the edible protein, it may suitably be obtained from limed bovine corium, i.e. the inner layer of the skin of male or female cattle, which has
SUBSTITUTE SHEET been dehaired and limed using standard commercial procedures. The material may be supplied as whole hide- sized pieces, or may be substituted by any other bovine corium material from any part of the whole hide, e.g. belly "splits", hide off-cuts. Other hide materials can be substituted for this raw material including the hides of any of the domestic meat animals, e.g. pig, sheep, deer, goat, chicken, turkey and other species commonly used for food in various parts of the world e.g. the skin of fish or kangaroo.
The polysaccharide is preferably film-forming and soluble. Examples include charged polysaccharides (e.g. pectin, alginates, agars, carageenans, and chitosan) , gums (e.g. arabic, acacia, tragacanth, locust bean and guar) , and modified celluloses (e.g. cellulose ethers such as methylcellulose, ethylcellulose, hydroxymethylcellulose, hydroxyethylcellulose, hydroxypropylmethylcellulose, hydroxypropylethylcellulose and carboxymethylcellulose) . Starches such as corn flour, crystal gum™, Dry-Flow™, and National Starch B38™ may alternatively be used. The preferred polysaccharide is hydroxypropylmethylcellulose (HPMC) .
The hydrophobic material should preferably be tasteless, odourless, solid at room temperatures, and pliable, resisting cracking and flaking when the coated film is manipulated. Suitable hydrophobic materials include edible oils and waxes, such as coconut oil, palm oil, palm kernel oil, acetylated monoglyceride (Dynacet) , glycerol monostearate, calcium and sodium steroyl lactate, polyglycerol ester and beeswax. Acetylated monoglyceride is preferred.
The film will generally contain protein in an amount of from 5 to 75%, more preferably from 15 to 35%, and most preferably from 20 to 30% by weight of protein plus polysaccharide. The film may additionally contain
SU ° plasticisers, flavourings, colourings and preservatives. The protein content of the uncoated film, including plasticisers and other components, will usually be from 3.5 to 60% by weight, more usually from 12 to 25% by weight, and most preferably from 15 to 22.5% by weight.
Suitable plasticisers include glycerol, sorbitol and polyethylene glycol, in amounts up to 40% by weight of the uncoated film. Preferably, the film contains plasticiser in an amount of from 5 to 30% (and more preferably from 20 to
30%) by weight of the uncoated film.
Flavourings for the film include artificial and naturally occurring flavours, spices and herbs. Suitable colourings include caramel and other permitted artificial or natural food dyes, and are generally employed in amounts less than 5% by weight of the uncoated film. Preservatives, such as propionic acid, sorbic acid, sodium nitrate and sodium nitrite, will usually constitute less than 1% by weight of the uncoated film.
The film may be formed by extrusion from a collagen/polysaccharide gel. The gel preferably has a solids content in the range 2 to 10%, and more preferably in the range 4 to 7%. After extrusion, the gel film is dried by any suitable means, such as by hot air. Preferably, the film is then brought up to a pH of from 6 to 8 by passage through an atmosphere of ammonia.
The hydrophobic material will generally be applied to the film in an amount of from 10 to 50 g/m2, and more preferably from 20 to 40 g/m2 of film surface, to produce a coating which is from 10 to 50 micrometers thick. Suitable coating techniques include dipping and brushing, but it is preferred to apply the coating by means of a heated roller or spray.
The films of the invention, and methods for their manufacture, are now further illustrated by reference to the following example, and to the Figures, in which:
Figure 1 is a graph showing the results of penetrometer studies of the pastry base of a quiche prepared with the film of the present invention, and
Figure 2 is a graph showing the effect of the film of the invention on the moisture content of quiche pastry.
EXAMPLE
1. Washing and decalcification of hides
Limed bovine corium (or other suitable collagen source) is placed in a large rotating vessel, e.g. a stainless steel Challenge-Cooke mixer or any other similar devices for freely mixing the raw material with water and other solvents to aid rapid washing/decalcification. Several deliming agents which remove chemically deposited and chemically bound lime by conversion into readily soluble salts can be utilized, e.g. ammonium sulphate, C02 deliming systems, hydrochloric acid, malic acid, acetic acid, lactic acid, citric acid-sodium citrate, or ammonium chloride.
The temperature of the system should be less than 20°C. The procedure is continued until the final liquor pH is approximately 4.5 - 5. The hides are then washed in water and drained. The washed hides may then be stored at 2 -10°C or deep frozen until required. The temperature of all solvents at all stages should be less than 20°C.
2. Grinding
The washed, decalcified and salted raw material is passed through a grinder for initial comminution. The whole pieces of corium are fed continuously into a grinding device such as a Weiler or Wolfking industrial food grinder. The
SUBSTITUTE SHEET material is passed through a plate or plates with 5mm-10mm holes such that 100% of the material is comminuted into approximately Smm-lOmm sized pieces of wet grind. The temperature of the material should be minimised at this stage. This wet grind is then transferred immediately to the next stage.
3. Comminution and mixing
The grind is pumped with water directly from the Wolfking or Weiler grinder to a hide and water holding tank. The resulting slurry is further comminuted by passing through Karl Schnell Mincemasters using plate sizes in the range of l-5mm or through a Stephan Microcut. The temperature rise is minimised at this stage and the resultant collagen pulp stored in the pulp holding tank. Food grade hydrochloric acid, glycerol, sorbitol and optionally aluminium sulphate are then charged to a second holding tank (Acid Tank) , together with water and ice. Suitable final concentrations in solution of these components are within indicated ranges:
hydrochloric acid .075 - 1.0% glycerol .5 - 1.0% sorbitol 4 - 6% aluminium sulphate .005 - .01%
The contents of the pulp tank and acid tank are blended together using a Stephan Microcut or similar high shear mixer or a Nauta mixer. The desired gel constituents are obtained and the resultant gel is stored in a blend tank for a minimum of 12 hours.
4. Preparation of collagen/polvsaccharide gel
The collagen gel thus obtained from the previous step is mixed in a Giusti pressure/mixing vessel, using iced water for cooling, with a solution of polysaccharide containing sufficient plasticiser to give a final solids content of 3.5% with a ratio of 25:75 collagen:polysaccharide by weight and the same final percentage of plasticiser as in the collagen only gel. Suitable polysaccharides include guar gum, locust bean gum, National Starch B38, crystal gum, "Dry-Flow", corn flour, methyl cellulose and hydroxypropyl methyl cellulose (HPMC) , preferably HPMC.
The resulting gel is homogenised using a Cherry Burrell homogeniser with automatic pressure control (34.5 ± 1.4 MPa, ie 5000 ± 200psi, with a minimal temperature rise) and passed into a line tank at a minimum of -730mm Hg via a deaerating distributor. The tank is pressurised to 270 kPa (2.7 Bar) and the gel then passed through two gel filters. Four filter banks are used to allow changing of gel filters - 2 for the first filter (placed in parallel) and 2 for the second filter (placed in parallel) . The first and second filters should be placed in series, and the gel filters should be capable of retaining particles greater than 0.076mm (0.003") .
5. Extrusion
The gel is transferred directly to an extruder. For extrusion, the gel is maintained at a maximum temperature of 19 ± 4°C) and extruded at 345 kPa (50 psi) onto a suitable conveyor, such as a PTFE (polytetrafluorethylene) coated glass fibre belt. The film is then batch-dried on the conveyor at 45°C for approximately 20 mins.
6. Hydrophobic coating
A hydrophobic layer is applied to one surface of the film using a heated roller loaded with the coating material, producing an even coating approximately 12.5 micrometres
(0.0005") thick. Materials tested were: coconut oil, beeswax, palm oil, palm kernel oil, acetylated monoglyceride
SUBSTITUTE-SHEET (Dynacet) , glycerol monostearate, calcium and sodium steroyl lactate and polyglycerol ester.
7. Cooking Trials
(i) Quiches
Quiches were prepared in 200 mm or 140 mm diameter aluminium moulds
Pastry ingredients: % w/w
Flour, soft plain white 58.7
Margarine 29.3 Water, chilled 11.7
Salt 0.3
Half the flour and all the margarine was blended in a food processor to form a smooth paste. The salt was • dissolved in the water and creamed into the mixture. The other half of the flour was added and the mixture processed to a homogeneous ball of pastry. 250g or 12Og of pastry was rolled by hand to 4mm thick and pressed into the mould and trimmed. The base of the pastry was pricked to prevent expansion of air bubbles distorting the pastry during cooking.
Filling ingredients: % w/w
Milk, skimmed 74.8
Eggs, whole 24.9
Salt 0.3
The milk was heated to 50°C and the eggs and salt beaten in. 330g or 200g (for smaller quiches) of filling was added to the raw pastry base. In the experimental quiches, the pastry base was first covered with the film of the invention, with the hydrophobic surface uppermost. The
SUBSTITUTE SHEET quiches were cooked in a preheated oven (190_ >C .) for 25 minutes, then the temperature reduced to 150°C for a further 15 minutes. The quiches were then removed, allowed to stand for 5 minutes, loosely covered with foil then chilled to 2°C in less than 90 minutes.
(ii)Meat Pies
Pastry was made to the recipe described above, and 1400mm diameter aluminium moulds were lined with 4mm thick rolled pastry. 200g of commercial tinned meat filling in gravy was added directly to the pastry shell or retained within an experimental film pouch prior to placing in the shell. A top crust (80g of pastry) was placed on top of the pie. Pies were baked at 175°C for 35-40 minutes, allowed to cool to room temperature, then chilled to 5°C.
8. Assessments
(i) Shrinkage
Any shrinkage of the film was detected visually on separation of the filling from the pastry base.
(ii) Penetrometer Studies
A characteristic of the pastry base which varies with moisture content is the resistance to deformation under applied pressure. This was measured in 50mm discs cut out of the pastry after removal of the filling, using a Lloyd tensile tester, type 5002, with an 8mm diameter probe attached to a 100 Newton load cell, crosshead speed 25mm per in. The characteristic of the stress/strain curve which was used was the peak height (Fig. 1) , corresponding to "firmness" or resistance to penetration; this was expressed as Newtons (N) .
S (iii) Moisture Content
The filling was separated from the pastry base and both were ground to homogeneity. lOg samples were weighed before and after heating at 80°C to constant weight (6h for pastry,
2Oh for filling) . 5 replicate samples were taken from each pie or quiche.
(iv) Sensory Assessment
A standard triangle taste for sensory difference was used with a randomly selected panel of 24 tasters. Samples of quiches were allocated random codes and the mode of presentation was balanced. Identification of one film- containing sample from two control samples was evaluated using the BS 5929, Part 1 (1980) test.
Results
(i) Film Production
No problems were encountered with the production of collagen/polysaccharide films; all those produced had sufficient mechanical strength and flexibility for handling.
(ii) Heat-sealing of Film
It was found possible to seal portions of pre-filling into film pouches, using a heated metal bar, prior to placing in the pie case.
(iii) Shrinkage on Cooking
Collagen film with no polysaccharide component shrank during cooking in quiches, exposing the pastry base and allowing penetration of moisture from the filling. However, inclusion of polysaccharide in the collagen film
SUBSTITUTE SHEET substantially reduced this thermal shrinkage: Methocel showed no detectable shrinkage during cooking in quiches.
(iv)Water Migration in Quiches
Examination of the pastry base typically showed three layers:
1. Closest to the filling was an opaque, white, soft, greasy layer.
2. A central layer which was white, dry and "crumbly" with small visible air spaces.
3. An outer layer, in contact with the cooking container, which was pale brown, dry and crumbly.
(a) Moisture Content
The migration of moisture from filling into the pastry base increased with time, illustrated by the change in water activity (Table 1) . This change was confirmed by measurement of moisture content (Figure 2, upper curve).
Incorporation of the film of the invention into quiches significantly reduced the rate of moisture migration into the pastry, determined by moisture content. The results of comparative tests involving the use of films coated with different hydrophobic materials are set out in Table 2. The best results were obtained with acetylated monoglyceride as the hydrophobic material. Not only was this most effective in reducing water migration, but it also had the best characteristics for application, adherence, flexibility, taste and mouthfeel, and it was therefore used for all subsequent tests.
A further series of comparative tests showed that a film comprising hydroxypropylmethylcellulose as the
SUBSTITUTE SHEET polysaccharide component was more effective as a moisture barrier than similar films containing alternative polysaccharides (Table 3) . HPMC was therefore used as the polysaccharide component in subsequent tests.
Figure 2 (lower curve) illustrates the reduced rate of water migration into the pastry base of a quiche in which the filling and the pastry base are separated by a film comprising collagen and HPMC, with a coating of acetylated monoglyceride.
(b) Pastry Crispness
The load/deformation characteristics of the pastry base measured on a tensile tester are shown in Figure 1. The three regions of the curve, A, B and C, are thought to correspond to the three layers of the cooked pastry, described above. The mean rupture load of the pastry decreased during storage, but the decrease was significantly less in quiches incorporating the film when compared with controls (Table 4).
(c) Taste Panel Assessments
The hedonic scores from a taste panel showed a clear improvement in "crispness" of the pastry in quiches with film (Table 5) . The scores indicate consistently higher "brittleness" and lower "softness" for the film-containing samples.
(v) Detectability of the Film
A taste panel assessment showed that a non-neutralised collagen film was detectable in quiches - due to its texture and "bitter" taste. However, a collagen/Methocel/Dynacet film which was neutralised after extrusion using ammonia was not detected by a significant proportion of tasters (10/24 compared with an expected 8/24 in the BS 5929 Part 1
SUBSTITUTE SHEET
Figure imgf000018_0001
16
"triangle" test, 1980) .
(vi) Effect of Film on Water Migration in Meat Pies
(a) Moisture Content
The moisture content of the base crust in control pies rose by 5.1% between 24 and 48h, whereas the moisture content of pies containing film rose only 0.7% (Table 6) . The top crusts, however, showed a similar rise in water content in control and film-containing pies.
(b) Load/Deformation Properties
The rupture-load of the top and base crusts were measured 24 and 48h after cooking. The pies containing film showed a significantly lower rupture load then controls in the top crusts at both 24 and 48h, but a higher rupture load for the base crust (Table 7) .
It will be appreciated that the present invention has been described above by way of example only, and that many variations are possible within the scope of the appendant claims.
SUBSTITUTE SHEET TABLE 1 Water activity* in σuiche (without film) during storage
Figure imgf000019_0001
* Decagon CX-1 water activity meter, 19.8 - 21.3°C
TABLE 2
Water uptake by pastry base of σuiche with different film coatings
Figure imgf000019_0002
SUBSTITUT TABLE 3
Water uptake bv pastry base of guiche with different polvsaccharides
Figure imgf000020_0001
TABLE 4
Force/deformation characteristics of quiche pastry during storage
Figure imgf000020_0002
cates significant difference from control (p < 0.05)
SUBSTITUTE SHEET TABLE 5 Taste panel hedonic scores for σuiches during storage
Figure imgf000021_0001
* the higher the score, the less acceptable the product
TABLE 6
Moisture content (%) of meat filled pies during storage
Figure imgf000021_0002
TABLE 7 Rupture loads for meat pie crusts during storage
Figure imgf000021_0003
* significantly different from control (p<0. 05 , n=6)
SUBSTITUTE SHEET

Claims

20CLAIMS
1. A film comprising an edible protein and an edible polysaccharide, said film having a coating of an edible hydrophobic material on at least a portion of a surface thereof.
2. A film according to claim 1 wherein said edible protein is a fibrous protein or a modified fibrous protein.
3. A film according to claim 2, wherein the fibrous protein is collagen.
4. A film according to any preceding claim, wherein the polysaccharide is selected from charged polysaccharides, gums and modified celluloses.
5. A film according to claim 4 wherein the polysaccharide is hydroxypropylmethylcellulose.
6. A film according to any preceding claim, wherein the hydrophobic material is an edible oil or wax.
7. A film according to claim 6 wherein the hydrophobic material is an esterified glyceride.
8. A film according to claim 7 wherein the esterified glyceride is acetylated monoglyceride.
9. A film according to any preceding claim wherein the film comprises from 3.5 to 60% protein, from 3.5 to 60% polysaccharide, and from 0 to 40% plasticiser, said percentages being by weight of the uncoated film.
10.A film according to any preceding claim wherein the hydrophobic material is present in an amount of from 10 to 50 g/m2.
SUBSTITUTE SHEET
11.A food product comprising a domain of comparatively high moisture content and a domain of lower moisture content, said domains having a film according to any preceding claim disposed therebetween.
12. food product according to claim 11 wherein the domain of lower moisture content comprises pastry.
SUBSTITUTE SHEET
PCT/GB1991/001244 1990-07-25 1991-07-25 Moisture barrier film WO1992001394A1 (en)

Priority Applications (6)

Application Number Priority Date Filing Date Title
JP03512374A JP3091487B2 (en) 1990-07-25 1991-07-25 Moisture barrier film
EP91913611A EP0550445B1 (en) 1990-07-25 1991-07-25 Moisture barrier film
AU82218/91A AU644463B2 (en) 1990-07-25 1991-07-25 Moisture barrier film
DE69110894T DE69110894T2 (en) 1990-07-25 1991-07-25 MOISTURE-RESISTANT FILM.
BR919106666A BR9106666A (en) 1990-07-25 1991-07-25 MOISTURE BARRIER FILM
GB9301414A GB2262245B (en) 1990-07-25 1993-01-25 Moisture barrier film

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB9016340.3 1990-07-25
GB909016340A GB9016340D0 (en) 1990-07-25 1990-07-25 Moisture barrier film

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EP0593123A1 (en) * 1992-10-16 1994-04-20 Latenstein Zetmeel B.V. Method of preparing a foil or coating on the basis of water insoluble proteins
GB2281187A (en) * 1993-08-12 1995-03-01 Convenience Foods Ltd Food product with edible moisture barrier layer
WO1996011577A1 (en) * 1994-10-13 1996-04-25 Unilever N.V. Pre-moulded, filled or topped dough systems
US5695800A (en) * 1996-03-13 1997-12-09 Viskase Corporation Method of preparing a food product encased in a glucomannan film
GB2321581A (en) * 1997-01-30 1998-08-05 Masterfoods Cv Two-in-one food packages
FR2766671A1 (en) * 1997-07-29 1999-02-05 Patrick Raulet Sa FRESH COMPOSITION COMPRISING FLOUR PASTE AND INTERIOR TRIM
EP0935921A1 (en) 1998-02-17 1999-08-18 Viskase Corporation Edible film and method
US6165521A (en) * 1997-01-29 2000-12-26 Arriba Corporation Food products utilizing edible films and method of making and packaging same
US6395320B1 (en) 1997-01-30 2002-05-28 Masterfoods, C.V. Two-component packaged food products
US6482240B1 (en) 1999-12-07 2002-11-19 Ed. Geistlich Soehne Ag Fur Chemische Industrie Method of making a collagen membrane from porcine skin
DE4343670C2 (en) * 1993-12-21 2003-05-28 Becker & Co Naturinwerk Edible serving for food
JP3476325B2 (en) 1997-02-06 2003-12-10 日世株式会社 Water-resistant biodegradable molded article and method for producing the same
WO2005063059A1 (en) * 2003-12-23 2005-07-14 Unilever N.V. Edible barrier
EP1586242A1 (en) * 2004-04-16 2005-10-19 Kraft Foods Holdings, Inc. Multilayer edible moisture barrier for food products
US7226629B2 (en) 2003-02-24 2007-06-05 Kraft Foods Holdings, Inc. Microwaveable grilled cheese and meat sandwiches and method of preparation
US7226630B2 (en) 2002-11-26 2007-06-05 Kraft Foods Holdings, Inc. Edible moisture barrier for food and method of use products
EP1875811A1 (en) * 2006-07-03 2008-01-09 Viscofan S.A. Chewable and/or edible product for pets and other animals
WO2008058649A1 (en) * 2006-11-11 2008-05-22 Lts Lohmann Therapie-Systeme Ag Consumable spice-containing film and also processes for production thereof
DE102007030732A1 (en) * 2007-07-02 2009-01-08 Roth, Erika Film wrapping, for sliced sausage and bread rolls, prevents the entry of moisture using an organic film material which is tasteless and edible
US7879384B2 (en) 2007-11-08 2011-02-01 Kraft Foods Global Brands Llc Structured glycerol esters useful as edible moisture barriers
US8206772B2 (en) 2007-11-08 2012-06-26 Kraft Foods Global Brands Llc Structured lipid compositions and methods of formulation thereof
WO2013089397A1 (en) * 2011-12-12 2013-06-20 C.L.Pharm Corporation Method and apparatus for manufacturing edible film product
US8486478B2 (en) 2007-11-08 2013-07-16 International Great Brands LLC Structured lipid compositions
CN109608702A (en) * 2018-12-26 2019-04-12 淮阴工学院 A kind of quinoa protein-Kujiang polysaccharide edible film and preparation method thereof

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EP0593123A1 (en) * 1992-10-16 1994-04-20 Latenstein Zetmeel B.V. Method of preparing a foil or coating on the basis of water insoluble proteins
GB2281187A (en) * 1993-08-12 1995-03-01 Convenience Foods Ltd Food product with edible moisture barrier layer
GB2281187B (en) * 1993-08-12 1995-09-06 Convenience Foods Ltd Food product
DE4343670C2 (en) * 1993-12-21 2003-05-28 Becker & Co Naturinwerk Edible serving for food
WO1996011577A1 (en) * 1994-10-13 1996-04-25 Unilever N.V. Pre-moulded, filled or topped dough systems
US5695800A (en) * 1996-03-13 1997-12-09 Viskase Corporation Method of preparing a food product encased in a glucomannan film
US6165521A (en) * 1997-01-29 2000-12-26 Arriba Corporation Food products utilizing edible films and method of making and packaging same
US6395320B1 (en) 1997-01-30 2002-05-28 Masterfoods, C.V. Two-component packaged food products
GB2321581A (en) * 1997-01-30 1998-08-05 Masterfoods Cv Two-in-one food packages
JP3476325B2 (en) 1997-02-06 2003-12-10 日世株式会社 Water-resistant biodegradable molded article and method for producing the same
EP0896798A1 (en) * 1997-07-29 1999-02-17 S.A. Patrick Raulet Filled dough products comprising a barrier layer
FR2766671A1 (en) * 1997-07-29 1999-02-05 Patrick Raulet Sa FRESH COMPOSITION COMPRISING FLOUR PASTE AND INTERIOR TRIM
EP0935921A1 (en) 1998-02-17 1999-08-18 Viskase Corporation Edible film and method
US7022358B2 (en) 1999-12-07 2006-04-04 Ed. Geistlich Sohne Ag Fur Chemische Industrie Collagen membrane made from porcine skin
US6482240B1 (en) 1999-12-07 2002-11-19 Ed. Geistlich Soehne Ag Fur Chemische Industrie Method of making a collagen membrane from porcine skin
US7226630B2 (en) 2002-11-26 2007-06-05 Kraft Foods Holdings, Inc. Edible moisture barrier for food and method of use products
US7229654B2 (en) 2002-11-26 2007-06-12 Kraft Foods Holdings, Inc. Multilayer edible moisture barrier for food products and method of use
US7226629B2 (en) 2003-02-24 2007-06-05 Kraft Foods Holdings, Inc. Microwaveable grilled cheese and meat sandwiches and method of preparation
WO2005063059A1 (en) * 2003-12-23 2005-07-14 Unilever N.V. Edible barrier
AU2004308061B2 (en) * 2003-12-23 2008-09-11 Unilever Plc Edible barrier
RU2373812C2 (en) * 2004-04-16 2009-11-27 Крафт Фудз Холдингс, Инк. Multi-layered edible moisture barrier for food products
EP1586242A1 (en) * 2004-04-16 2005-10-19 Kraft Foods Holdings, Inc. Multilayer edible moisture barrier for food products
AU2005201450B2 (en) * 2004-04-16 2010-12-16 Kraft Foods Group Brands Llc Multilayer edible moisture barrier for food products
EP1875811A1 (en) * 2006-07-03 2008-01-09 Viscofan S.A. Chewable and/or edible product for pets and other animals
ES2303446A1 (en) * 2006-07-03 2008-08-01 Viscofan, S.A. Chewable and/or edible product for pets and other animals
ES2303446B1 (en) * 2006-07-03 2009-07-28 Viscofan, S.A. MASSABLE AND / OR EDIBLE PRODUCT FOR PETS AND ANIMALS.
WO2008058649A1 (en) * 2006-11-11 2008-05-22 Lts Lohmann Therapie-Systeme Ag Consumable spice-containing film and also processes for production thereof
DE102007030732A1 (en) * 2007-07-02 2009-01-08 Roth, Erika Film wrapping, for sliced sausage and bread rolls, prevents the entry of moisture using an organic film material which is tasteless and edible
US7879384B2 (en) 2007-11-08 2011-02-01 Kraft Foods Global Brands Llc Structured glycerol esters useful as edible moisture barriers
US8206772B2 (en) 2007-11-08 2012-06-26 Kraft Foods Global Brands Llc Structured lipid compositions and methods of formulation thereof
US8486478B2 (en) 2007-11-08 2013-07-16 International Great Brands LLC Structured lipid compositions
US8911813B2 (en) 2007-11-08 2014-12-16 Intercontinental Great Brands Llc Structured lipid compositions
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CN109608702B (en) * 2018-12-26 2021-05-25 淮阴工学院 Quinoa protein-atrina pectinata polysaccharide edible film and preparation method thereof

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CA2087948A1 (en) 1992-01-26
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BR9106666A (en) 1993-06-08
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